2016
DOI: 10.1016/j.fluid.2016.08.025
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Vapor – Liquid equilibria study of the ternary systems containing sucrose in aqueous solutions of ionic liquids, 1-butyl-3-methyl imidazolium bromide and 1-hexyl-3-methyl imidazolium bromide at 298.15 K and atmospheric pressure

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Cited by 27 publications
(33 citation statements)
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“…This behavior is consistent with the results obtained from vapor-liquid equilibrium behavior of {sucrose / fructose + [BMIm]Br / [HMIm]Br + water} systems in regard with sugar-ionic liquid interactions. 15,16 Our results are also consistent with the volumetric and viscometric results obtained by Shekaari and coworkers. 31 They studied density and viscosity of ternary {D-xylose + ionic liquids 1-hexyl-3-methyl imidazolium bromide or 1-octyl-3methyl imidazolium bromide or 1-decyl-3methylimidazoliume bromide + water} systems.…”
Section: Resultssupporting
confidence: 92%
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“…This behavior is consistent with the results obtained from vapor-liquid equilibrium behavior of {sucrose / fructose + [BMIm]Br / [HMIm]Br + water} systems in regard with sugar-ionic liquid interactions. 15,16 Our results are also consistent with the volumetric and viscometric results obtained by Shekaari and coworkers. 31 They studied density and viscosity of ternary {D-xylose + ionic liquids 1-hexyl-3-methyl imidazolium bromide or 1-octyl-3methyl imidazolium bromide or 1-decyl-3methylimidazoliume bromide + water} systems.…”
Section: Resultssupporting
confidence: 92%
“…To achieve this goal, a systematic study of thermophysical properties is required. In this work, in continuation to our previous papers, [13][14][15][16][17][18][19][20] the solubility values of galactose in aqueous ionic liquids, 1-butyl-3-methyl imidazolium bromide, [BMIm]Br, 1-hexyl-3-methyl imidazolium bromide, [HMIm]Br and 1-butyl-3-methylimidazolium chloride [BMIm]Cl have been measured at different ionic liquid mole fractions at T = (298.15 and 308.15) K using the gravimetric method. To model the experimental solubility data of galactose in water and aqueous ionic liquid solutions, models such as Wilson, 21 NRTL, 22 modified NRTL, 23 NRF-NRTL 24 and UNIQUAC 25 were used.…”
Section: Introductionsupporting
confidence: 64%
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